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US Patent 10233138 Process for preparing ethylene glycol from a carbohydrate source

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Is a
Patent
Patent

Patent attributes

Patent Jurisdiction
United States Patent and Trademark Office
United States Patent and Trademark Office
Patent Number
10233138
Date of Patent
March 19, 2019
Patent Application Number
15543116
Date Filed
January 13, 2016
Patent Citations Received
‌
US Patent 12077489 Continuous, carbohydrate to ethylene glycol processes
0
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US Patent 11319269 Continuous processes for the selective conversion of aldohexose-yielding carbohydrate to ethylene glycol using low concentrations of retro-aldol catalyst
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US Patent 11319268 Continuous, carbohydrate to ethylene glycol processes
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US Patent 11919840 Methods for operating continuous, unmodulated, multiple catalytic step processes
0
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US Patent 10472310 Continuous processes for the highly selective conversion of sugars to propylene glycol or mixtures of propylene glycol and ethylene glycol
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US Patent 10544072 Continuous processes for the highly selective conversion of aldohexose-yielding carbohydrate to ethylene glycol
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US Patent 10988426 Continuous processes for the highly selective conversion of aldohexose-yielding carbohydrate to ethylene glycol
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US Patent 11680031 Continuous processes for the selective conversion of aldohexose-yielding carbohydrate to ethylene glycol using low concentrations of retro-aldol catalyst
0
Patent Primary Examiner
‌
Pancham Bakshi
Patent abstract

Ethylene glycol is prepared from a carbohydrate source in a process,wherein hydrogen, the carbohydrate source, a liquid diluent and a catalyst system are provided as reactants into a reaction zone;wherein the catalyst system comprises a tungsten compound and at least one hydrogenolysis metal selected from the noble metals Pd, Pt, Ru, Rh, Ir and combinations thereof;wherein the carbohydrate source is introduced into the reaction zone such that in the reaction zone the concentration of the carbohydrate source in the diluent is at least 4% wt, calculated as weight of carbohydrate source per weight of diluent;wherein the amount of the at least one hydrogenolysis metal selected from the noble metals Pd, Pt, Ru, Rh, Ir and combinations thereof ranges from 0.2 to 1.0% wt, calculated as the metal and based on the amount of carbohydrate source introduced into the reaction zone;wherein the molar ratio of tungsten to the at least one hydrogenolysis metal is in the range of 1 to 25; andwherein the carbohydrate source is reacted with hydrogen in the presence of the catalyst system to yield an ethylene glycol-containing product.

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